JPH0376173B2 - - Google Patents
Info
- Publication number
- JPH0376173B2 JPH0376173B2 JP59157790A JP15779084A JPH0376173B2 JP H0376173 B2 JPH0376173 B2 JP H0376173B2 JP 59157790 A JP59157790 A JP 59157790A JP 15779084 A JP15779084 A JP 15779084A JP H0376173 B2 JPH0376173 B2 JP H0376173B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- tank
- storage tank
- working
- pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000007788 liquid Substances 0.000 claims description 94
- 230000005484 gravity Effects 0.000 claims description 20
- 238000012545 processing Methods 0.000 claims description 14
- 239000003085 diluting agent Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 3
- 238000007865 diluting Methods 0.000 claims 1
- 239000000243 solution Substances 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000012141 concentrate Substances 0.000 description 8
- XYXNTHIYBIDHGM-UHFFFAOYSA-N ammonium thiosulfate Chemical group [NH4+].[NH4+].[O-]S([O-])(=O)=S XYXNTHIYBIDHGM-UHFFFAOYSA-N 0.000 description 6
- 238000005259 measurement Methods 0.000 description 5
- 238000005086 pumping Methods 0.000 description 5
- 239000004480 active ingredient Substances 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- G—PHYSICS
- G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
- G03D—APPARATUS FOR PROCESSING EXPOSED PHOTOGRAPHIC MATERIALS; ACCESSORIES THEREFOR
- G03D3/00—Liquid processing apparatus involving immersion; Washing apparatus involving immersion
- G03D3/02—Details of liquid circulation
- G03D3/06—Liquid supply; Liquid circulation outside tanks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/48—Mixing liquids with liquids; Emulsifying characterised by the nature of the liquids
- B01F23/483—Mixing liquids with liquids; Emulsifying characterised by the nature of the liquids using water for diluting a liquid ingredient, obtaining a predetermined concentration or making an aqueous solution of a concentrate
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/8593—Systems
- Y10T137/85954—Closed circulating system
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/8593—Systems
- Y10T137/85978—With pump
- Y10T137/86035—Combined with fluid receiver
- Y10T137/86067—Fluid sump
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Accessories For Mixers (AREA)
Description
【発明の詳細な説明】
本発明は混合液製造の方法と装置に関する。特
に本発明は濃厚液と稀釈液から稀溶液の製造に関
するが、それのみでなく混和性液体混合物が要求
される場合にも応用できるものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for producing a mixed liquid. In particular, the present invention relates to the production of dilute solutions from concentrates and dilute solutions, but is also applicable where miscible liquid mixtures are required.
多くの製造法や物質を液体中で処理する多くの
方法において、予め定めた濃度の処理液を出来る
限り正確迅速に製造する必要がある。多くの場合
液体は浴から蒸発、反応により又は浴をとおる物
質に運ばれて損失するので処理液浴と処理液浴を
補足するための同濃度の補充液浴を製造すること
が多くの場合必要となる。特にシート材料を処理
液浴中にとおす様な場合にこのような必要が生ず
る。 BACKGROUND OF THE INVENTION In many manufacturing methods and in many methods for processing substances in liquids, it is necessary to produce processing liquids of predetermined concentrations as accurately and quickly as possible. Because liquid is often lost from the bath by evaporation, reaction, or transport to materials passing through the bath, it is often necessary to produce a process liquid bath and a replenisher bath of the same concentration to supplement the process liquid bath. becomes. This need arises particularly when the sheet material is passed through a bath of processing liquid.
2浴の製造には4液の測定を要する。2液は濃
厚液であり2液は稀釈液である。濃厚液が強アル
カリ性、強酸性又は健康上危険なものであるなら
ば、濃厚液について多くの測定を行なうことは誠
に好ましくない。 The production of two baths requires the measurement of four liquids. The second liquid is a concentrated liquid and the second liquid is a diluted liquid. It is really undesirable to carry out many measurements on a concentrated liquid if the concentrated liquid is strongly alkaline, strongly acidic or hazardous to health.
更に濃厚液を稀釈液と混合する場合も稀釈液全
容量中、稀液又は濃液部分がない様均一濃度にす
ることは極めてむずかしい。 Furthermore, when a concentrated liquid is mixed with a diluted liquid, it is extremely difficult to achieve a uniform concentration so that there is no diluted liquid or concentrated liquid part in the entire volume of the diluted liquid.
米国特許第4002267号に濃厚液と稀釈液からの
溶液の製法が記載されている。この方法では濃厚
液は単一容器に入れられている。容器内容物を供
給タンクに接続している管中にあけ同時に稀釈液
の測定量を同じ管に送り供給タンク中で稀溶液を
製造する。これは複雑な配管と稀釈液の極めて正
確な測量手段を必要とする。更に稀液体が供給タ
ンク中で十分混合されたかどうか確認する手段が
ない。 US Pat. No. 4,002,267 describes a method for preparing solutions from concentrates and dilute solutions. In this method, the concentrate is contained in a single container. The contents of the container are poured into a tube connected to a supply tank and at the same time a measured amount of diluent solution is sent into the same tube to produce a dilute solution in the supply tank. This requires complex piping and highly accurate means of gauging the diluent. Furthermore, there is no way to check whether the dilute liquid has been sufficiently mixed in the supply tank.
本発明の目的は処理浴とそれに伴なう補充浴と
の液混合物を両液を測定する必要なく容易に製造
できる方法と装置を提供することにある。また装
置内の液を均一濃度にする方法及び装置が提供さ
れる。 SUMMARY OF THE INVENTION An object of the present invention is to provide a method and apparatus that can easily produce a liquid mixture of a processing bath and an accompanying replenishment bath without the need to measure both liquids. A method and apparatus are also provided for making the liquid within the apparatus uniform in concentration.
本発明によれば装置中の貯槽に濃厚液の必要量
を加え、次に貯槽の液水準が貯槽の立上り管の頂
部に達する迄貯槽に稀釈液を加え更に連続添加し
て貯槽中の過剰液を立上り管をとおして接続した
作業槽に流し、作業槽中の稀釈液量が予定量に達
した時稀釈液添加を止めた後作業槽の底から少な
くとも1部の液を引出し貯槽中にポンプ送液し貯
槽中の過剰液は作業槽中に流れさせ貯槽と作業槽
の液比重が同一となるまで作業槽から貯槽へのポ
ンプ送液をつづけることより成る処理装置中の作
業濃度溶液の製法が提供される。 According to the present invention, the required amount of concentrated liquid is added to the reservoir in the apparatus, and then the diluent is added to the reservoir until the liquid level in the reservoir reaches the top of the riser pipe of the reservoir, and the excess liquid in the reservoir is continuously added. is poured into the connected working tank through the riser pipe, and when the amount of diluent in the working tank reaches the predetermined amount, the diluent addition is stopped, and at least part of the liquid is drawn out from the bottom of the working tank and pumped into the storage tank. A method for producing a working concentration solution in a processing device, which consists of pumping the liquid, allowing the excess liquid in the storage tank to flow into the working tank, and continuing pumping the liquid from the working tank to the storage tank until the specific gravity of the liquid in the storage tank and the working tank become the same. is provided.
好ましくは、予めパツクされ、量が測定された
濃厚液が貯槽に加えられる。 Preferably, a pre-packed and measured amount of concentrate is added to the reservoir.
作業槽から貯槽へのポンプ送液開始前に2槽中
および同一槽のちがつた部分でさえその比重がか
なりちがつて濃厚液と稀釈剤が十分混合されてい
ないことを示していることがわかつた。しかしポ
ンプの数分運転後は2槽およびそれらの各部の液
比重が均一に近づく。更にポンプによる作業槽か
ら貯槽への液循環後は各槽およびその各部分の液
比重は同一となり濃厚液と稀釈液の完全混合がで
きたことがわかる。 Before pumping from the working tank to the storage tank began, it was found that the specific gravities in the two tanks and even in different parts of the same tank were significantly different, indicating that the concentrate and diluent were not sufficiently mixed. Ta. However, after several minutes of operation of the pump, the liquid specific gravity of the two tanks and their respective parts approaches uniformity. Furthermore, after the liquid was circulated from the working tank to the storage tank by the pump, the specific gravity of the liquid in each tank and each part thereof became the same, indicating that the concentrated liquid and diluted liquid were completely mixed.
本発明の他の態様によれば処理装置中に貯槽中
の過剰液を作業槽に流れさす様作業槽に接続して
いる溢流立上り管を中にもつ貯槽、処理液を用い
て物質を処理できる作業槽、貯槽へ稀釈液を加え
る手段、作業槽中にある液水準表示手段、作業槽
底から貯槽底に液を送るため連結されている液体
ポンプおよび液の比重測定手段より成る濃厚液と
稀釈液から作業濃度処理液を製造する装置が提供
される。 According to another aspect of the invention, a storage tank having an overflow riser therein connected to a working tank for directing excess liquid in the storage tank to a working tank in a processing apparatus, wherein the processing liquid is used to process material. A concentrated liquid comprising a working tank capable of producing a concentrated liquid, a means for adding diluent to the storage tank, a liquid level display means in the working tank, a liquid pump connected to convey the liquid from the bottom of the working tank to the bottom of the storage tank, and a means for measuring the specific gravity of the liquid. An apparatus is provided for producing a working concentration processing solution from a diluent solution.
付図は本発明を例示するに役立つであろう。 The accompanying figures will serve to illustrate the invention.
図1〜5はすべて本発明に使われる装置の断面
図でありまた各図中の同一番号は同一部分を示す
ものである。 1 to 5 are all cross-sectional views of the apparatus used in the present invention, and the same numbers in each figure indicate the same parts.
図1は液貯槽1と処理液作業槽2より成る空の
装置を示している。濃厚液とこの例では水である
稀釈液は貯槽1で混合された後、作業槽2に送ら
れて活性成分の予め定めた濃度液を作業槽2中に
つくり、そして貯槽1中には作業槽2の液補充に
使用できる活性成分の同一濃度の液をつくる。 FIG. 1 shows an empty apparatus consisting of a liquid storage tank 1 and a processing liquid working tank 2. As shown in FIG. The concentrate and the diluent, which in this example is water, are mixed in reservoir 1 and then sent to working tank 2 to create a predetermined concentration of active ingredient in working tank 2; Create a solution with the same concentration of active ingredient that can be used to replenish tank 2.
貯槽1には給水管3があり上部の開いた立上り
管4は管5によつて作業槽2の底に接続してい
る。作業槽2中に液面スイツチ7があり液面が予
定高さに達した時に稀釈水を止める。 The storage tank 1 has a water supply pipe 3, and an open riser pipe 4 is connected to the bottom of the working tank 2 by a pipe 5. A liquid level switch 7 is provided in the working tank 2 to stop the dilution water when the liquid level reaches a predetermined height.
管8は2槽1と2の底を連絡している。管8中
にポンプ9があり、これは槽1から2へもまた槽
2から1へも液を送ることができる。 A pipe 8 connects the bottoms of the two tanks 1 and 2. In the tube 8 there is a pump 9, which is capable of pumping liquid both from tank 1 to tank 2 and from tank 2 to tank 1.
槽2の右に浮秤11を入れた広口びん10があ
り、浮秤は液比重測定に使用する。 On the right side of the tank 2 is a wide mouth bottle 10 containing a floating scale 11, which is used to measure the specific gravity of the liquid.
図1では槽1と2はいずれも液が入つていな
い。図2では包装容器から貯槽1に注入された予
め定めた量の濃厚液Cが入つている。その量は立
上り管4の高さの中途迄となつている。 In FIG. 1, both tanks 1 and 2 contain no liquid. In FIG. 2, a predetermined amount of concentrated liquid C is poured into a storage tank 1 from a packaging container. The amount is approximately halfway up the height of the riser pipe 4.
図3において稀釈水Dが給水管3から出てい
る。水Dは一部濃厚液Cと混合し液量が増すので
過剰液は立上り管4を流下し作業槽2に入る。こ
の2槽中の液はC+Dといい、不完全混合を示し
ている。 In FIG. 3, dilution water D is coming out from the water supply pipe 3. Part of the water D mixes with the concentrated liquid C and the liquid volume increases, so that the excess liquid flows down the riser pipe 4 and enters the working tank 2. The liquids in these two tanks are called C+D, indicating incomplete mixing.
図4では作業槽2中の液面を必要高さとするに
十分な水Dが流入している。液面スイツチ7が働
いて給水が停止している。 In FIG. 4, enough water D is flowing in to raise the liquid level in the working tank 2 to the required height. The liquid level switch 7 is activated and the water supply is stopped.
この段階では槽1と2はいずれも不完全混合液
C+Dを入れている。 At this stage, both tanks 1 and 2 contain incompletely mixed liquid C+D.
次いでポンプ9によつて液を槽2から1に送り
槽1の過剰液は立上り管4をへて槽2に流れかく
て槽2の液面が保たれる。 Liquid is then pumped from tank 2 to tank 1 by pump 9, and excess liquid in tank 1 flows through riser pipe 4 to tank 2, thereby maintaining the liquid level in tank 2.
次いで広口びん10と浮秤11を使つて2槽の
液比重を測定する。2液の比重が一致した時ポン
プ9を止める。 Next, the liquid specific gravity of the two tanks is measured using a wide mouth bottle 10 and a floating scale 11. When the specific gravities of the two liquids match, the pump 9 is stopped.
両槽1と2が完全混合された作業濃度処理済液
Mを入れている状態が図5に示されている。 FIG. 5 shows a state in which both tanks 1 and 2 contain completely mixed working concentration treated liquid M.
作業槽2中で物質が処理される様な操作によつ
てこの槽から液が取去られる。液面指示計7が作
動した場合ポンプ9は働いて槽1から槽2に液を
送つてこの槽の液面を保つ。 Liquid is removed from the working tank 2 by such an operation that the material is treated in this tank. When the liquid level indicator 7 operates, the pump 9 operates to send liquid from tank 1 to tank 2 to maintain the liquid level in this tank.
1操作において図1〜5の装置は作業濃度の写
真定着液の製造に使われまた写真印画紙は作業槽
2で定着された。 In one operation, the apparatus of FIGS. 1-5 was used to produce a working strength photographic fixer and photographic paper was fixed in working tank 2.
この場合定着液の主活性成分はチオ硫酸アンモ
ニウムである。 The main active component of the fixer in this case is ammonium thiosulfate.
市販チオ硫酸アンモニウム濃厚液は687.2g/
を含み比重1.335であつた。 Commercially available ammonium thiosulfate concentrate is 687.2g/
The specific gravity was 1.335.
作業濃度溶液中のチオ硫酸アンモニウム濃度は
137.44g/である必要があり、その比重は
1.076である。 The concentration of ammonium thiosulfate in the working concentration solution is
It needs to be 137.44g/, and its specific gravity is
It is 1.076.
図2に示す槽1に濃厚チオ硫酸塩溶液C3を
入れ図4に示すとおり水Dを加え液C+Dの全量
を15とした。 Concentrated thiosulfate solution C3 was placed in tank 1 shown in FIG. 2, and water D was added as shown in FIG. 4 to make the total volume of solution C+D 15.
かくて2槽の液中のチオ硫酸アンモニウムの理
論濃度は必要濃度である137.44g/であつた。 Thus, the theoretical concentration of ammonium thiosulfate in the liquid in the two tanks was the required concentration of 137.44 g/.
しかし比重測定は実際濃度が2槽中でまた各槽
のちがつた部分中でかなり変動していることを示
した。 However, specific gravity measurements showed that the actual concentration varied considerably in the two tanks and in different parts of each tank.
1試験においてポンプ運転開始前図4に示す状
態において比重測定結果次のとおりであつた:
比重
槽2 頂部 1.082
槽2 底部 1.112
槽1 頂部 1.030
槽1 底部 1.100
液を槽2から槽1にポンプで5分間送つた後の
比重は次のとおりとなつた:
槽2 頂部 比重1.074
槽2 底部 1.080
槽1 頂部 1.070
槽1 底部 1.070
ポンプ運転12分後比重は次のとおりになつた:
槽2 頂部 比重1.076
槽2 底部 1.076
槽1 頂部 1.076
槽1 底部 1.076
これは濃チオ硫酸アンモニウム溶液が正確に水
と混合されて装置全体にチオ硫酸アンモニウム
137.44g/の均一作業濃度液となつたことを示
している。この結果は槽1と2両方の液Mの化学
分析によつて確認された。 In one test, the specific gravity was measured in the state shown in Figure 4 before pump operation started, and the results were as follows: Density tank 2 top 1.082 Tank 2 bottom 1.112 Tank 1 top 1.030 Tank 1 bottom 1.100 The liquid was pumped from tank 2 to tank 1. After pumping for 5 minutes, the specific gravity was as follows: Tank 2 Top Specific Gravity 1.074 Tank 2 Bottom 1.080 Tank 1 Top 1.070 Tank 1 Bottom 1.070 After 12 minutes of pump operation, the specific gravity was as follows: Tank 2 Top Specific Gravity 1.076 Tank 2 Bottom 1.076 Tank 1 Top 1.076 Tank 1 Bottom 1.076 This is because the concentrated ammonium thiosulfate solution is precisely mixed with water and the entire device is filled with ammonium thiosulfate.
This shows that the solution had a uniform working concentration of 137.44 g/g/. This result was confirmed by chemical analysis of liquid M from both tanks 1 and 2.
一般操作において装置全体にわたり一定の比重
測定値をえるに必要な時間が特定濃厚液を用いて
一旦確立されたならばこの混合時間は毎回使用で
き比重測定は必要ない。 Once the time necessary to obtain a constant specific gravity measurement throughout the apparatus in general operation is established with a particular concentrate, this mixing time can be used every time and specific gravity measurements are not required.
図1から5まではいずれも本発明に使われる装
置の概略断面図である。図1は装置が空の状態、
図2は濃厚液Cを入れた状態、図3はCに稀釈液
Dを加えつつあり、図4はDの添加完了の状態、
図5は均一混合液Mとなつた状態である。
1……貯槽、2……作業槽、3……稀釈液供給
管、4……立上り溢流管、9……ポンプ。
1 to 5 are schematic cross-sectional views of the apparatus used in the present invention. Figure 1 shows the empty state of the device.
Figure 2 shows the state in which concentrated liquid C has been added, Figure 3 shows the state in which diluted liquid D is being added to C, and Figure 4 shows the state in which addition of D has been completed.
FIG. 5 shows a state in which a uniform mixed liquid M has been obtained. 1... Storage tank, 2... Working tank, 3... Diluent supply pipe, 4... Rising overflow pipe, 9... Pump.
Claims (1)
貯槽中の液面が貯槽中の立上り管の頂部に達する
迄貯槽に稀釈液を加え更に貯槽に稀釈液添加をつ
づけて貯槽の過剰液を立上り管を経て連絡する作
業槽に流れさせ、作業槽中の液量が予定量に達し
た時稀釈液供給流を中止した後ポンプの運転を開
始し液の少なくとも1部を作業槽の底から貯槽に
送り貯槽の過剰液を作業槽に流れさせかつ貯槽と
作業槽内の液比重が同一となる迄作業槽から貯槽
へのポンプ送液をつづけることより成ることを特
徴とする処理装置中の作業濃度液の製法。 2 予めパツクされ、量を測定してある濃厚液を
貯槽に加える特許請求の範囲第1項に記載の方
法。 3 溢流立上り管4をもつ液体貯槽1、貯槽1内
の過剰液が流れる様立上り管に接続しており、か
つ処理用液を用いて物質を処理する作業槽2、貯
槽に稀釈液を供給する部材3、作業槽2内にある
液面表示部材7、作業槽2の底から貯槽の底に連
絡している送液ポンプ9および液体比重測定計1
1より成ることを特徴とする濃厚液からの作業濃
度処理液製造装置をもつ物質処理用装置。[Claims] 1. Adding a necessary amount of concentrated liquid to a storage tank in a processing device,
Add diluting solution to the storage tank until the liquid level in the storage tank reaches the top of the riser pipe in the storage tank, and then continue adding diluent to the storage tank to cause excess liquid in the storage tank to flow through the riser pipe to the communicating work tank. When the amount of liquid in the tank reaches the predetermined amount, the diluent supply flow is stopped and the pump is started to pump at least a portion of the liquid from the bottom of the working tank to the storage tank, allowing excess liquid in the storage tank to flow into the working tank. A method for producing a working concentration liquid in a processing device, which comprises continuing to pump liquid from the working tank to the storage tank until the specific gravity of the liquid in the storage tank and the working tank become the same. 2. The method according to claim 1, wherein a pre-packed and measured amount of concentrated liquid is added to the storage tank. 3. A liquid storage tank 1 having an overflow riser pipe 4, a working tank 2 connected to the riser pipe so that excess liquid in the storage tank 1 can flow, and in which a substance is treated using a processing liquid, and a diluent solution supplied to the storage tank. a liquid level display member 7 in the working tank 2, a liquid feeding pump 9 communicating from the bottom of the working tank 2 to the bottom of the storage tank, and a liquid specific gravity measuring meter 1.
1. An apparatus for material processing having an apparatus for producing a working concentration processing liquid from a concentrated liquid, characterized by comprising:
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8321794 | 1983-08-12 | ||
GB838321794A GB8321794D0 (en) | 1983-08-12 | 1983-08-12 | Solution mixing apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6054727A JPS6054727A (en) | 1985-03-29 |
JPH0376173B2 true JPH0376173B2 (en) | 1991-12-04 |
Family
ID=10547236
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59157790A Granted JPS6054727A (en) | 1983-08-12 | 1984-07-30 | Method and device for mixing solution |
Country Status (5)
Country | Link |
---|---|
US (1) | US4650339A (en) |
EP (1) | EP0134199B1 (en) |
JP (1) | JPS6054727A (en) |
DE (1) | DE3466087D1 (en) |
GB (1) | GB8321794D0 (en) |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62622A (en) * | 1985-06-27 | 1987-01-06 | Kokusan Denki Co Ltd | Controller for internal-combustion engine |
JP2684099B2 (en) * | 1989-10-20 | 1997-12-03 | 富士重工業株式会社 | 2-tank fuel tank device |
US5289223A (en) * | 1990-11-23 | 1994-02-22 | Gunter Woog | Chemical recycler for photo processing machine |
US5057858A (en) * | 1990-11-23 | 1991-10-15 | Gunter Woog | Developer recycler in connection with photo processing machine |
US5317360A (en) * | 1990-11-23 | 1994-05-31 | Gunter Woog | Chemical recycler for photo processing machine |
US5054519A (en) * | 1990-12-26 | 1991-10-08 | Imtec Products, Inc. | Recirculating chemical bath with inflow and self balancing outflow |
GB2278864B (en) * | 1993-06-10 | 1996-07-17 | James Leslie Dallas | System for retrieving waste drilling mud |
US6269831B1 (en) | 1998-03-31 | 2001-08-07 | E. I. Du Pont De Nemours And Company | Precision volumetric measuring and mixing apparatus |
CN1157504C (en) * | 2000-03-21 | 2004-07-14 | 亚洲电镀器材有限公司 | Mixing device |
CN1314502A (en) | 2000-03-21 | 2001-09-26 | 亚洲电镀器材有限公司 | Mixing device |
US20030037824A1 (en) * | 2001-07-16 | 2003-02-27 | Aubin Denis John | Enhanced fluid motion |
EP1400846A1 (en) * | 2002-09-20 | 2004-03-24 | Agfa-Gevaert AG | Circulation device |
US11319944B2 (en) | 2003-10-30 | 2022-05-03 | Deka Products Limited Partnership | Disposable interconnected pump cassettes having first and second pump chambers with valved inlet and outlet connections |
US7354190B2 (en) * | 2003-10-30 | 2008-04-08 | Deka Products Limited Partnership | Two-stage mixing system, apparatus, and method |
US8158102B2 (en) * | 2003-10-30 | 2012-04-17 | Deka Products Limited Partnership | System, device, and method for mixing a substance with a liquid |
US7662139B2 (en) * | 2003-10-30 | 2010-02-16 | Deka Products Limited Partnership | Pump cassette with spiking assembly |
ATE463775T1 (en) * | 2007-03-08 | 2010-04-15 | Special Coating Lab Internat S | DEVICE FOR CONTROLLING THE CONCENTRATION OF A COMPONENT IN A LIQUID |
EP2555859B1 (en) * | 2010-04-08 | 2014-09-10 | Sintokogio, Ltd. | A circulating-type dispersing system and a method therefor |
EP4389872A2 (en) | 2015-10-09 | 2024-06-26 | DEKA Products Limited Partnership | Fluid pumping and bioreactor system |
US11299705B2 (en) | 2016-11-07 | 2022-04-12 | Deka Products Limited Partnership | System and method for creating tissue |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1917577A (en) * | 1928-11-26 | 1933-07-11 | Jr William A Doble | Fuel mixer |
US4096066A (en) * | 1969-07-05 | 1978-06-20 | Kearney T J | Treating contaminated liquids |
DE2323160A1 (en) * | 1973-05-08 | 1974-11-28 | Agfa Gevaert Ag | METHOD AND DEVICE FOR MIXING |
US4506986A (en) * | 1982-10-04 | 1985-03-26 | Ciba-Geigy Ag | Method and apparatus for preparating liquid mixtures |
-
1983
- 1983-08-12 GB GB838321794A patent/GB8321794D0/en active Pending
-
1984
- 1984-07-30 JP JP59157790A patent/JPS6054727A/en active Granted
- 1984-08-06 DE DE8484810385T patent/DE3466087D1/en not_active Expired
- 1984-08-06 EP EP84810385A patent/EP0134199B1/en not_active Expired
-
1986
- 1986-02-14 US US06/829,855 patent/US4650339A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS6054727A (en) | 1985-03-29 |
EP0134199B1 (en) | 1987-09-09 |
US4650339A (en) | 1987-03-17 |
DE3466087D1 (en) | 1987-10-15 |
EP0134199A1 (en) | 1985-03-13 |
GB8321794D0 (en) | 1983-09-14 |
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